Journal
ADVANCED POWDER TECHNOLOGY
Volume 29, Issue 12, Pages 3257-3264Publisher
ELSEVIER SCIENCE BV
DOI: 10.1016/j.apt.2018.09.004
Keywords
Dual layer granular bed filter; Filtration efficiency; Pressure drop; Semi-coke powder; Coal pyrolysis
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Funding
- K. C. Wong Magna Fund of Ningbo University
- National 863 High Technology Research Program of China [2008AA05Z205]
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The separation of semi-coke powders from tars and gases during coal pyrolysis is of crucial importance to the coal chemical industry. This work describes an experimental study on semi-coke powder filtration using an experimental dual layer granular bed filter with an inner diameter of 100 mm. With an initial filtration velocity of 0.2 m/s, the dual layer granular bed filter had a filtration efficiency of 99.943% and a pressure drop across the filter of only 1456 Pa. When the initial filtration velocity was increased to 0.25 m/s, the filtration efficiency was 99.937% and the pressure drop was 1834 Pa. Our results indicated that the dual layer granular bed filter we developed and tested showed significant promise as a high-temperature dust collector in low-temperature coal pyrolysis. (C) 2018 The Society of Powder Technology Japan. Published by Elsevier B.V. and The Society of Powder Technology Japan. All rights reserved.
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